EP2528998A2 - Gasification reactor and process - Google Patents

Gasification reactor and process

Info

Publication number
EP2528998A2
EP2528998A2 EP11700693A EP11700693A EP2528998A2 EP 2528998 A2 EP2528998 A2 EP 2528998A2 EP 11700693 A EP11700693 A EP 11700693A EP 11700693 A EP11700693 A EP 11700693A EP 2528998 A2 EP2528998 A2 EP 2528998A2
Authority
EP
European Patent Office
Prior art keywords
blast
blaster
syngas
gas
quench
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP11700693A
Other languages
German (de)
French (fr)
Other versions
EP2528998B1 (en
EP2528998B8 (en
Inventor
Thomas Paul Von Kossak-Glowczewski
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Air Products and Chemicals Inc
Original Assignee
Shell Internationale Research Maatschappij BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to EP11700693.2A priority Critical patent/EP2528998B8/en
Priority to PL11700693T priority patent/PL2528998T3/en
Publication of EP2528998A2 publication Critical patent/EP2528998A2/en
Publication of EP2528998B1 publication Critical patent/EP2528998B1/en
Application granted granted Critical
Publication of EP2528998B8 publication Critical patent/EP2528998B8/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/485—Entrained flow gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/52—Ash-removing devices
    • C10J3/526—Ash-removing devices for entrained flow gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
    • C10J3/845—Quench rings
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/093—Coal

Definitions

  • the present invention relates to a gasification reactor and a process for the production of syngas by gasification of a carbonaceous feed, wherein the reactor comprises a gasifier unit with a discharge channel for discharging a stream of slag-loaded hot syngas and a quencher for supplying a flow of quench gas into the discharge channel.
  • carbonaceous feedstock such as pulverized coal
  • a reactor In gasification processes for the production of synthetic gas, or syngas, carbonaceous feedstock, such as pulverized coal, is partially oxidised in a reactor.
  • the syngas typically has a temperature of 1300 - 1600°C.
  • the hot syngas contains liquid slag droplets . In order to avoid fouling on the heat
  • quench gas This recycled cooled gas is generally referred to as quench gas.
  • EP 0 347 986 Al discloses an interchangeable quench gas injection ring with nozzles injecting cooled and recycled gas into the raw gas product as it leaves the reactor.
  • the recycled cooled gas should be mixed into the hot syngas uniformly and a film of cool gas should be formed adjacent the wall where the supply line of the quench gas exits into the gas stream.
  • the hot syngas stream In operation, the hot syngas stream, typically flowing in upward direction, forms stalagmites and vertical upstanding beards of deposited slag where it is mixed with the cooled recycled gas. These slag deposits disturb the gas flow. If these deposits grow too large, the desired cool gas film cannot be obtained anymore and the cooled gas is mixed unevenly within the hot gas flow.
  • the object of the invention is to provide an effective way to prevent large slag deposits at the point where the quench gas is mixed into the hot gas flow.
  • the object is achieved with a gasification reactor for the production of syngas by gasification of a carbonaceous feed, wherein the reactor comprises a discharge channel for discharging a stream of slag-loaded hot syngas and a quencher for supplying a flow of quench gas into the discharge channel, wherein at least one blaster is arranged comprising at least one blast nozzle in line with the flow direction of the quench gas.
  • blast nozzle is in line with the flow direction of the quench gas, it is able to blast away slag deposits possibly hindering the quench gas flow. It does not mean that the blast
  • the at least one blaster can for example be
  • a source of pressurized blast gas selected from the group of syngas, nitrogen, carbon dioxide, steam and mixtures thereof.
  • the blaster is divided into a plurality of compartments, each comprising one or more blast lances, whereby an even number of opposite compartments is operated symmetrically to mitigate the blast impulse into the center of the discharged syngas stream.
  • the blaster can for example be divided into 4 - 16 compartments, for example 8 compartments, each compartment comprising a number of blast lances.
  • the slag beards typically grow on the upper
  • the quench area typically has a bottom sloping downwardly in the direction of the opening and making an acute angle with the horizontal, resulting in a sharp peripheral edge between the reactor and the quench area. If the blasted slag beards leave some remaining slag deposit on this peripheral edge, these residual deposits can initiate growth of new slag beards. In order to hinder this, the slag deposits should preferably be blasted away
  • the blaster can be directed to this upper peripheral edge of the reactor.
  • the blaster is preferably directed to blast under a blast angle which is 0,1 - 5 degrees steeper than the flow direction of the quench gas, which is
  • the blaster can comprise a number of blast lances extending in the radial direction of the discharge channel with an angle of 1 - 3 degrees between adjacent lances.
  • the at least one blaster can for instance be operated periodically.
  • the pressure of the blast gas can, e.g., be kept 10 - 100 bar higher than the pressure of the discharged syngas.
  • the gas can be blasted into the quench area with a velocity of, for example, 30 - 300 m/s .
  • the blasters can be operated to release a continuous purge flow in addition to the periodically released blast flow. This also has the advantage that the blaster tips are cooled and protected against heat radiation from the syngas.
  • Figure 1 shows schematically a longitudinal cross section of a gasification reactor according to the present invention
  • Figure 2 shows in detail a radial cross section of a quench section of the reactor of Figure 1;
  • Figure 3 shows in plan view the quench area of the reactor of Figure 1.
  • the gasification reactor 1 shown in Fig. 1 comprises a gasifier unit 2 in a vertically oriented elongated pressure container 3.
  • the gasifier unit 2 is supplied with a carbonaceous feed, for example pulverized coal, which is partially combusted by a number of burners (not shown) in the gasifier unit 2 to form syngas.
  • a carbonaceous feed for example pulverized coal
  • the gasifier unit 2 At its top end the gasifier unit 2 comprises an opening 15 which opens into a quench area 18.
  • the quench area 18 has a slightly sloping bottom 19 around the opening 15 forming an acute upper peripheral edge 16.
  • the quench area 18 forms the beginning of a discharge channel 4.
  • a quench gas supply unit 5 is arranged to mix cool quench gas into the stream A of discharged hot syngas to cool down the syngas to below the softening point of the slag particles carried by the discharged syngas .
  • Quenched syngas flows from the quench gas supply unit 5 in quench gas flow direction B (see Figure 2) into the discharge channel 4 and further downstream the quench gas supply unit 5 transporting the hot syngas to heat exchangers (not shown) for further cooling.
  • the quench gas supply unit 5 comprises radially extending quench gas supply channels 6 in a circular arrangement coaxial with the discharge channel 4 and the gasifier unit 2.
  • the quench gas supply channels 6 have an open end 7 directed towards the center line X of the discharge channel 4, while their other end is connected to a quench gas supply line 8. From the supply line 8 to the open end 7, the supply channels 6 slope downwardly.
  • the reactor 1 is further provided with a blaster 10, as shown in more detail in Figure 2 and in plan view in Figure 3.
  • the blaster 10 is built of eight compartments 11. Each compartment 11 comprises a plurality of radially
  • Each blast lance 12 makes an angle of about 2 degrees with the adjacent blast lance 12, resulting in an average distance of about 11 mm.
  • the blast lances 12 are directed to blast in a direction C (see Figure 2) in line with the quench flow direction B, so as to blast away slag deposits standing in the way of the quench gas flow B.
  • the blaster 10 is directed to blast under an angle a with the sloping bottom 19 of the quench area 18. The angle a is
  • the slag deposits are particularly formed on the upper peripheral edge 16 at the top end of the gasifier unit 2. When the slag beards are blasted away, they may leave some remaining slag deposit on this peripheral edge 16, which can initiate growth of new slag beards. In order to hinder this, the slag deposits should preferably be blasted away completely without leaving any residue.
  • the blaster 10 in this embodiment is directed to this upper peripheral edge 16 of the gasifier unit 2.
  • Each blast lance 12 is connected to a source of pressurized blast gas via a circular distribution line 13 which is connected to a supply line 14.
  • the blast lances can blast the gas with a velocity of 30 - 300 m/ s .
  • the pressure of the blast gas is 10 - 100 bar higher than the pressure of the discharged syngas. Pairs of opposite compartments 11 are operated symmetrically to mitigate the blast impulse into the center X of the discharged syngas stream.
  • the blaster 10 is operated periodically to blast away slag deposits around the top end opening of the gasifier unit 2, where the hot syngas is cooled by the quench gas.
  • the blaster 10 further releases a continuous purge flow in addition to the periodically released blast flow .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Industrial Gases (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Processing Of Solid Wastes (AREA)
  • Furnace Details (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A gasification reactor (1) and a process for the production of syngas by gasification of a carbonaceous feed. The reactor comprises a gasifier unit with a discharge channel (4) for discharging a stream of slag-loaded hot syngas and a quencher (5) for supplying a flow of quench gas into the discharge channel (4). At least one blaster (10) is arranged comprising at least one blast nozzle (12), such as a blast lance, in line with the flow direction of the quench gas. The blaster (10) can be connected to a source of pressurized gas, such as syngas, nitrogen, carbon dioxide, steam or the like. The blaster can be actuated periodically to blast away slag deposits.

Description

GASIFICATION REACTOR AND PROCESS
The present invention relates to a gasification reactor and a process for the production of syngas by gasification of a carbonaceous feed, wherein the reactor comprises a gasifier unit with a discharge channel for discharging a stream of slag-loaded hot syngas and a quencher for supplying a flow of quench gas into the discharge channel.
In gasification processes for the production of synthetic gas, or syngas, carbonaceous feedstock, such as pulverized coal, is partially oxidised in a reactor.
Initially, the syngas typically has a temperature of 1300 - 1600°C. The hot syngas contains liquid slag droplets . In order to avoid fouling on the heat
exchangers, it is necessary to solidify the liquid slag droplets that are entrained in the gas leaving the gasifier, and to cool the liquid slag droplets to a temperature at which they are not sticky. This means that the entire gas stream leaving the gasifier must be cooled to a temperature that is well below the slag softening temperature. To this end, the hot syngas leaving the reactor is quenched to temperatures between 1000 - 700°C by feeding back cleaned and cooled syngas into the gas stream before it is transported to one or more heat exchangers. This recycled cooled gas is generally referred to as quench gas.
EP 0 347 986 Al discloses an interchangeable quench gas injection ring with nozzles injecting cooled and recycled gas into the raw gas product as it leaves the reactor. The recycled cooled gas should be mixed into the hot syngas uniformly and a film of cool gas should be formed adjacent the wall where the supply line of the quench gas exits into the gas stream.
In operation, the hot syngas stream, typically flowing in upward direction, forms stalagmites and vertical upstanding beards of deposited slag where it is mixed with the cooled recycled gas. These slag deposits disturb the gas flow. If these deposits grow too large, the desired cool gas film cannot be obtained anymore and the cooled gas is mixed unevenly within the hot gas flow.
The object of the invention is to provide an effective way to prevent large slag deposits at the point where the quench gas is mixed into the hot gas flow.
The object is achieved with a gasification reactor for the production of syngas by gasification of a carbonaceous feed, wherein the reactor comprises a discharge channel for discharging a stream of slag-loaded hot syngas and a quencher for supplying a flow of quench gas into the discharge channel, wherein at least one blaster is arranged comprising at least one blast nozzle in line with the flow direction of the quench gas.
This way, slag deposits can effectively be removed by activating the blaster. Since the blast nozzle is in line with the flow direction of the quench gas, it is able to blast away slag deposits possibly hindering the quench gas flow. It does not mean that the blast
direction must be strictly parallel to the quench flow direction .
The at least one blaster can for example be
connected to a source of pressurized blast gas selected from the group of syngas, nitrogen, carbon dioxide, steam and mixtures thereof.
In a particular embodiment, the blaster is divided into a plurality of compartments, each comprising one or more blast lances, whereby an even number of opposite compartments is operated symmetrically to mitigate the blast impulse into the center of the discharged syngas stream. The blaster can for example be divided into 4 - 16 compartments, for example 8 compartments, each compartment comprising a number of blast lances. By activating two opposite blaster compartments, symmetrical blasting can be achieved without the need to activate all blast lances simultaneously.
The slag beards typically grow on the upper
peripheral edge of the gasifier unit where it opens into the gas discharge channel and where the hot syngas is quenched with the cool quench gas in a quench area. The quench area typically has a bottom sloping downwardly in the direction of the opening and making an acute angle with the horizontal, resulting in a sharp peripheral edge between the reactor and the quench area. If the blasted slag beards leave some remaining slag deposit on this peripheral edge, these residual deposits can initiate growth of new slag beards. In order to hinder this, the slag deposits should preferably be blasted away
completely without leaving any residue. To this end, the blaster can be directed to this upper peripheral edge of the reactor. The blaster is preferably directed to blast under a blast angle which is 0,1 - 5 degrees steeper than the flow direction of the quench gas, which is
substantially parallel to the sloping bottom of the quench area.
For effective cleaning, the blaster can comprise a number of blast lances extending in the radial direction of the discharge channel with an angle of 1 - 3 degrees between adjacent lances. The at least one blaster can for instance be operated periodically. In order to blast the blast gas with optimum velocity, the pressure of the blast gas can, e.g., be kept 10 - 100 bar higher than the pressure of the discharged syngas. The gas can be blasted into the quench area with a velocity of, for example, 30 - 300 m/s .
To keep the blast nozzles open and free the blasters can be operated to release a continuous purge flow in addition to the periodically released blast flow. This also has the advantage that the blaster tips are cooled and protected against heat radiation from the syngas.
An exemplary embodiment of the invention will now be described by reference to the accompanying drawing, in which:
Figure 1: shows schematically a longitudinal cross section of a gasification reactor according to the present invention;
Figure 2: shows in detail a radial cross section of a quench section of the reactor of Figure 1;
Figure 3 : shows in plan view the quench area of the reactor of Figure 1.
The gasification reactor 1 shown in Fig. 1 comprises a gasifier unit 2 in a vertically oriented elongated pressure container 3. The gasifier unit 2 is supplied with a carbonaceous feed, for example pulverized coal, which is partially combusted by a number of burners (not shown) in the gasifier unit 2 to form syngas. At its top end the gasifier unit 2 comprises an opening 15 which opens into a quench area 18. The quench area 18 has a slightly sloping bottom 19 around the opening 15 forming an acute upper peripheral edge 16. The quench area 18 forms the beginning of a discharge channel 4. In the quench area 18 a quench gas supply unit 5 is arranged to mix cool quench gas into the stream A of discharged hot syngas to cool down the syngas to below the softening point of the slag particles carried by the discharged syngas . Quenched syngas flows from the quench gas supply unit 5 in quench gas flow direction B (see Figure 2) into the discharge channel 4 and further downstream the quench gas supply unit 5 transporting the hot syngas to heat exchangers (not shown) for further cooling. The quench gas supply unit 5 comprises radially extending quench gas supply channels 6 in a circular arrangement coaxial with the discharge channel 4 and the gasifier unit 2. The quench gas supply channels 6 have an open end 7 directed towards the center line X of the discharge channel 4, while their other end is connected to a quench gas supply line 8. From the supply line 8 to the open end 7, the supply channels 6 slope downwardly.
When the discharged hot syngas is cooled down by the quench gas to a temperature below the softening point of the slag particles, these slag particles are deposited to form upstanding stalagmites 17, as shown in Figure 2.
Near the quench supply unit 6 the reactor 1 is further provided with a blaster 10, as shown in more detail in Figure 2 and in plan view in Figure 3. The blaster 10 is built of eight compartments 11. Each compartment 11 comprises a plurality of radially
extending blast lances 12. Each blast lance 12 makes an angle of about 2 degrees with the adjacent blast lance 12, resulting in an average distance of about 11 mm.
The blast lances 12 are directed to blast in a direction C (see Figure 2) in line with the quench flow direction B, so as to blast away slag deposits standing in the way of the quench gas flow B. The blaster 10 is directed to blast under an angle a with the sloping bottom 19 of the quench area 18. The angle a is
preferably 0,1 - 5 degrees.
The slag deposits are particularly formed on the upper peripheral edge 16 at the top end of the gasifier unit 2. When the slag beards are blasted away, they may leave some remaining slag deposit on this peripheral edge 16, which can initiate growth of new slag beards. In order to hinder this, the slag deposits should preferably be blasted away completely without leaving any residue.
To this end, the blaster 10 in this embodiment is directed to this upper peripheral edge 16 of the gasifier unit 2.
Each blast lance 12 is connected to a source of pressurized blast gas via a circular distribution line 13 which is connected to a supply line 14. The blast lances can blast the gas with a velocity of 30 - 300 m/ s . The pressure of the blast gas is 10 - 100 bar higher than the pressure of the discharged syngas. Pairs of opposite compartments 11 are operated symmetrically to mitigate the blast impulse into the center X of the discharged syngas stream.
The blaster 10 is operated periodically to blast away slag deposits around the top end opening of the gasifier unit 2, where the hot syngas is cooled by the quench gas. The blaster 10 further releases a continuous purge flow in addition to the periodically released blast flow .

Claims

C L A I M S
1. A gasification reactor (1) for the production of syngas by gasification of a carbonaceous feed, wherein the reactor comprises a gasifier unit (2) with a
discharge channel (4) for discharging a stream of slag- loaded hot syngas and a quencher (5) for supplying a flow of quench gas into the discharge channel (4), wherein at least one blaster (10) is arranged comprising at least one blast nozzle (12) in line with the flow direction (B) of the quench gas and wherein blaster (10) is directed to the upper edge (16) of the syngas outlet of gasifier unit
(2) of the reactor (1) where the gasifier unit (2) opens into the discharge channel (4) .
2. A gasification reactor according to claim 1 wherein the at least one blaster (10) is connected to a source of pressurized gas selected from the group of syngas, nitrogen, carbon dioxide, steam and mixtures thereof.
3. A gasification reactor according to any one of the preceding claims, wherein the at least one blaster (10) is arranged to blast the gas with a velocity of 30 - 300 m/s.
4. A gasification reactor according to any one of the preceding claims wherein the blaster (10) is divided into a plurality of compartments (11), each comprising one or more blast lances (12), whereby an even number of opposite compartments is operated symmetrically to mitigate the blast impulse into the center of the discharged syngas stream.
5. A gasification reactor according to claim 4, wherein the blaster is divided into 4 - 16 compartments (11), each compartment comprising a number of blast lances (12) .
6. A gasification reactor according to any one of the preceding claims wherein the quencher (5) is located in a quench area (18) with a bottom sloping downwardly to the upper edge (16) of the gasifier unit and wherein the blaster (10) is directed to blast under a blast angle which is 0,1 - 5 degrees steeper than the sloping bottom of the quench area (18) .
7. A gasification reactor according to any one of the preceding claims wherein the blaster (10) comprises a number of blast lances (12) extending in the radial direction of the discharge channel (4) with an angle of 1 - 3 degrees between adjacent lances.
8. A process for the production of syngas by
gasification of a carbonaceous feed in a reactor (1) comprising a gasifier unit (2) opening into a discharge channel (4) for discharging a stream of slag-loaded hot syngas and a quencher (5) for supplying a flow of quench gas into the discharge channel (4), wherein at least one blaster (10) comprising at least one blast nozzle (12) directed in line with the flow direction of the quench gas is operated periodically.
9. A process according to claim 8 wherein the pressure of the blast gas is 10 - 100 bar higher than the pressure of the discharged syngas.
10. A process according to claim 8 or 9 wherein at least a part of the blasters (10) is operated to release a continuous purge flow in addition to the periodically released blast flow.
EP11700693.2A 2010-01-25 2011-01-25 Gasification reactor and process Active EP2528998B8 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP11700693.2A EP2528998B8 (en) 2010-01-25 2011-01-25 Gasification reactor and process
PL11700693T PL2528998T3 (en) 2010-01-25 2011-01-25 Gasification reactor and process

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP10151517 2010-01-25
PCT/EP2011/050986 WO2011089268A2 (en) 2010-01-25 2011-01-25 Gasification reactor and process
EP11700693.2A EP2528998B8 (en) 2010-01-25 2011-01-25 Gasification reactor and process

Publications (3)

Publication Number Publication Date
EP2528998A2 true EP2528998A2 (en) 2012-12-05
EP2528998B1 EP2528998B1 (en) 2018-09-19
EP2528998B8 EP2528998B8 (en) 2018-11-14

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US (1) US9234147B2 (en)
EP (1) EP2528998B8 (en)
JP (1) JP2013518139A (en)
KR (1) KR101865029B1 (en)
CN (1) CN102725382B (en)
AU (1) AU2011208638B2 (en)
PL (1) PL2528998T3 (en)
WO (1) WO2011089268A2 (en)
ZA (1) ZA201204754B (en)

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CN108799822B (en) * 2018-06-15 2020-04-17 绿城农科检测技术有限公司 Nitrogen continuous gas supply system
CN110358582B (en) * 2019-01-15 2023-12-26 新能能源有限公司 Pulverized coal hydro-gasification device
CN113072980B (en) * 2021-04-28 2021-12-07 宁夏神耀科技有限责任公司 Downward full waste boiler entrained flow bed gasification equipment of superheated steam and coal chemical system

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PL2528998T3 (en) 2019-04-30
WO2011089268A2 (en) 2011-07-28
AU2011208638B2 (en) 2014-04-03
CN102725382B (en) 2014-08-13
CN102725382A (en) 2012-10-10
ZA201204754B (en) 2013-02-27
AU2011208638A1 (en) 2012-07-19
EP2528998B1 (en) 2018-09-19
WO2011089268A3 (en) 2011-12-29
EP2528998B8 (en) 2018-11-14
JP2013518139A (en) 2013-05-20
KR101865029B1 (en) 2018-06-07
US20120292573A1 (en) 2012-11-22
US9234147B2 (en) 2016-01-12
KR20120127431A (en) 2012-11-21

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